U.S. patent number 3,576,078 [Application Number 05/007,815] was granted by the patent office on 1971-04-27 for paper drying process and apparatus.
This patent grant is currently assigned to Consolidated Papers, Inc.. Invention is credited to Sherwood G. Holt.
United States Patent |
3,576,078 |
Holt |
April 27, 1971 |
PAPER DRYING PROCESS AND APPARATUS
Abstract
A process and apparatus for drying webs of newly formed paper
material in the dryer section of a paper making machine having a
plurality of rotatable dryer drums over which the paper web is
guided in seriatim in heat exchange relationship while the web is
disposed between open mesh dryer fabric endless belting and the web
is scrubbed by air circulated through the meshes of the fabric
while moving beneath hoods embracing the dryer drums.
Inventors: |
Holt; Sherwood G. (Wisconsin
Rapids, WI) |
Assignee: |
Consolidated Papers, Inc.
(Wisconsin Rapids, WI)
|
Family
ID: |
21728261 |
Appl.
No.: |
05/007,815 |
Filed: |
February 2, 1970 |
Current U.S.
Class: |
34/454;
34/114 |
Current CPC
Class: |
D21F
5/02 (20130101) |
Current International
Class: |
D21F
5/00 (20060101); D21F 5/02 (20060101); F26b
003/00 () |
Field of
Search: |
;34/23,114,159 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Dority, Jr.; Carroll B.
Claims
I claim:
1. In apparatus for drying a paper web in the dryer section of a
paper making machine, a plurality of drums rotating about
horizontal axes arranged in upper and staggered lower series, a
pair of porous fabric belts for embracing engagement with the
opposed faces of said paper web and for conveying the web in spaced
relationship to and alternately about said dryer drums, and dryer
hood means embracing a plurality of said dryer drums in
substantially the area where the paper web is carried thereover,
said hoods including dryer air supply inlets and exhausts and means
for causing turbulence of the air while passing said hoods and for
subjecting the paper web to air scrubbing action through the meshes
of said porous fabric.
2. The apparatus of claim 1 wherein each of said drying drums
include an embracing dryer hood.
3. The apparatus of claim 1 wherein said dryer fabric belts are of
varying permeability in the cross direction, the permeability being
greatest adjacent its longitudinal center.
4. In a method for drying a paper web in the dryer section of a
paper making machine comprising a plurality of horizontally
disposed rotatable dryer drums arranged in upper and staggered
lower series the steps which comprise moving the paper web between
a pair of porous fabric belts alternately about said dryer drums,
and simultaneously subjecting the paper web to air scrubbing action
through the meshes of said porous fabric by impinging and flowing
air thereover in a turbulent manner while being conveyed about said
dryer drums.
Description
This invention relates to improvements in the process and apparatus
for drying paper webs in the drying section of a paper making
machine having a plurality of drums rotating about horizontal axes
over which the paper web is guided seriatim in heat exchange
relationship.
In the typical dryer section of a paper making machine, heated
drying drums are arranged in horizontally disposed upper and
staggered lower series and the web is conducted sequentially into
contact with the drum in one of the series to a drum in the other
of the series and back to the first series and so on. An endwise
flexible woven fabric belt or dryer felt has heretofore been
conventionally associated with each of the series of dryer drums,
that is, a dryer belt is arranged to press the web into heat
exchange relationship with a peripheral portion of each of the
dryer drums with the opposed sides of the paper web alternately
embracing the drums in the respective upper and lower series.
The evaporation rates obtained with present-day "Can" type dryers
or drying drums of the aforesaid class is about 1 to 2 pounds per
hour per square foot. This can be contrasted with drying rates of
from about 20 to about 40 pounds per hour per square foot obtained
with the relatively large diameter "Yankee" drums, the latter being
characterized by a diameter of from about 9 to about 15 feet. This
higher rate for the Yankee dryers is partially due to better
conduction of heat from the dryer shell to the adhering paper, but
is mostly due to employment therewith of high velocity types of
hoods which reduces the boundary layer film of moist air to a
minimum which thus increases mass surfaces. A considerable amount
of heat is also transmitted to the sheet from this "scrubbing"
air.
In the arrangement of the present invention, the paper sheet to be
dried is carried over the surfaces of the dryer drums between an
opposed pair of open mesh dryer fabrics and subjected to scrubbing
action through the meshes of the fabric by means of air caused to
flow in a turbulent manner through hoods which embrace
approximately one-half of the periphery of said drying drums at the
area where the paper web is caused to pass over said drums.
Although the presence of this fabric tends to retard evaporation,
the thickness of the boundary layer film can be reduced to
approximately 0.020 inch In contrast to this, in a conventional
system employing dense conveyor felts where almost no evaporation
takes place over the dryer surface, the boundary layer in the open
sheet draws in the neighborhood of 0.25 inch. With the arrangement
of the present invention the drying rate can be in the neighborhood
of 8 pounds per hour per square foot representing a four-fold
increase. Although no increase in heat transfer from the cylinder
to the sheet would be expected, this can also be increased by
heating the scrubbing air in the hoods.
The present invention is particularly useful in overcoming problems
encountered in dryer sections as speeds are increased above 2,000
feet per minute and basis weight of paper is less than 26 pounds
per 3,000 square feet. Thus, in the present invention where the
sheet is essentially sandwiched between two porous fabrics which
follow the normal sheet run through the dryer section, the
arrangement is self-threading and avoids the problem of sheet
flutter and windage which are becoming problems for high weight
paper grades.
With the present arrangement the sheet is separated from the dryer
surfaces by a porous fabric at all times. While this will decrease
the transfer of heat from the drying drum to the sheet, this
decrease can be compensated for by the scrubbing air. Moreover, in
the drying of lightweight paper, overall drying ability is not
critical.
Perhaps one of the most valuable benefits from such a system is the
tendency of the dryer section to level out cross machine
nonuniformities of moisture. While the present "Can" dryers have
this same tendency, however, this will be greatly increased by the
high velocity air impingement employed in the present invention.
Wetter spots, having better conductivity and better opportunity for
vapor transfer, will dry more rapidly than the drier spots.
Although drying hoods of conventional character can be employed in
the present invention, the use of porous dryer fabrics of varying
permeability in a cross direction have been found particularly
useful, such drying fabrics consisting of endless belts of flexible
woven fabric whereof the warp threads are greater in number per
linear inch adjacent the longitudinal edges of the belts and
decrease in number therefrom in a crosswise direction towards the
longitudinal center of the belt, whereby the humidity profile,
during drying, is flattened to produce a more uniform drying across
the paper machine width. The porous fabric between which the paper
web is confined and carried about the drying drums can be composed
of either conventional cotton or asbestos or synthetic fabric such
as polyester fiber or nylon and wherein the cross threads may be
monofilaments and the warp threads of spun fibers.
The process and apparatus of the present invention, its details and
arrangements will be apparent from a consideration of the following
specification and accompanying drawings, wherein the drawing
diagrammatically illustrates the dryer section of a paper making
machine embodying the present invention.
Referring to the drawings, a fragmentary portion of the dryer
section of a paper making machine is illustrated and comprises a
plurality of heated drying cylinders, drums or cans 10 arranged in
horizontally disposed upper and staggered lower series with the
paper web 11 conducted sequentially into contact with a drum in one
of the series to a drum in the other of the series and then back to
the first series and so on, as is conventional so that heat is
passed to the paper web from the drum in alternate directions a
plurality of times until the web is dried to the desired
extent.
While the paper web 11 is being carried over the drying drums in
the manner aforesaid, it is conducted thereover between the porous
fabrics 12 and 13 which are in the form of endless belts usually in
separate pairs, which eliminate sheet marking due to the fabric
contour or a series of pairs of fabrics operating as separate
sections, the speeds of which can be adjusted to allow for stretch
or shrinkage, one going about the upper cylinders and one going
about the lower cylinders, with conventional tensioning by
intermediate pocket rolls (not shown) which guide the fabrics 12
and 13 in its passage about the drying cylinders 10.
As the paper sheet 11 is guided about the cylinder 10, it is
further enveloped by a driving hood such as that shown at either
14, 15 or 16 of FIG. 1. While three different types of drying hoods
are illustrated, it will be understood that generally one type of
drying hood will be employed in a single dryer section and that
hoods are similarly provided for the lower row of drying drums in
inverted position. These dryer hoods embrace about one-half of the
periphery of the drying cylinders and have an arcuate top wall 17
as shown in the dryer 14, or the angular wall 18 for the dryer 15,
or the composite wall 19 for the dryer 16. An air supply, either
room temperature or preferably heated air, is introduced at a high
velocity to the various drying hoods such as for example into the
supply conduit 20 and through the hood 14 wherein a turbulent flow
is induced to the air supply be means of the undulating member 21
and exhausted through the conduit 22. Air may be supplied to and
exhausted from each air hood individually or two or more adjacent
hoods may be connected to each other so that the air supply flows
through a plurality of hoods.
In the hood 15 air turbulence is provided by means of a
convergent-divergent channel defined by the convergent and
divergent components of the wall or or enclosure 18, and in the
hood 16 a turbulent flow of air is provided to the supply plenum 23
and emitted through the exhaust plenum 24. The foregoing various
types of hood designs per se are conventional and known to have the
general effect of reducing boundary layer thickness.
Although I have shown and described the preferred embodiment of my
invention, it will be understood by those skilled in the art that
changes may be made in the details thereof without departing from
its scope as comprehended by the following claims.
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